| Kinetic modeling of the oxidative dehydrogenation of ethane to ethylene over a MoVTeNbO catalytic system G Che-Galicia, R Quintana-Solórzano, RS Ruiz-Martínez, JS Valente, ... Chemical Engineering Journal 252, 75-78, 2014 | 97 | 2014 |
| Modeling of oxidative dehydrogenation of ethane to ethylene on a MoVTeNbO/TiO2 catalyst in an industrial-scale packed bed catalytic reactor G Che-Galicia, RS Ruiz-Martínez, F López-Isunza, CO Castillo-Araiza Chemical Engineering Journal 280, 682-694, 2015 | 72 | 2015 |
| Engineering considerations to produce bioactive compounds from plant cell suspension culture in bioreactors EA Motolinía-Alcántara, CO Castillo-Araiza, M Rodríguez-Monroy, ... Plants 10 (12), 2762, 2021 | 60 | 2021 |
| Kinetics of HDS and of the inhibitory effect of quinoline on HDS of 4, 6-DMDBT over a Ni–Mo–P/Al2O3 catalyst: Part I JC García-Martínez, CO Castillo-Araiza, JA De los Reyes Heredia, E Trejo, ... Chemical Engineering Journal 210, 53-62, 2012 | 59 | 2012 |
| Kinetic assessment of the simultaneous hydrodesulfurization of dibenzothiophene and the hydrogenation of diverse polyaromatic structures EM Morales-Valencia, CO Castillo-Araiza, SA Giraldo, ... ACS Catalysis, 2018 | 57 | 2018 |
| Heat-transfer studies in packed-bed catalytic reactors of low tube/particle diameter ratio CO Castillo-Araiza, H Jiménez-Islas, F López-Isunza Industrial Engineering Chemical Research 46 (23), 7426-7435, 2007 | 53 | 2007 |
| Hydrodynamic models for packed beds with low tube-to-particle diameter ratio CO Castillo-Araiza, F López-Isunza International Journal of Chemical Reactor Engineering 6 (A1), 1-14, 2008 | 47 | 2008 |
| Modeling the partial oxidation of o-xylene in an industrial packed bed catalytic reactor: the role of hydrodynamics and catalyst activity in the heat transport CO Castillo-Araiza, F López-Isunza Industrial Engineering Chemical Research 49, 6845–6853, 2010 | 45 | 2010 |
| A simple approach to describe hydrodynamics and its effect on heat and mass transport in an industrial wall-cooled fixed bed catalytic reactor: ODH of ethane on a MoVNbTeO … G Aparicio-Mauricio, RS Ruiz, F López-Isunza, CO Castillo-Araiza Chemical Engineering Journal 321, 584-599, 2017 | 40 | 2017 |
| Kinetic Assessment of the Dry Reforming of Methane over a Ni–La2O3 Catalyst VS Sandoval-Bohorquez, EM Morales-Valencia, CO Castillo-Araiza, ... Acs Catalysis 11 (18), 11478-11493, 2021 | 37 | 2021 |
| Cadmium (II), lead (II), and copper (II) biosorption on Baker’s yeast (Saccharomyces cerevesiae) A Dutta, L Zhou, CO Castillo-Araiza, E De Herdt Journal of Environmental Engineering 142 (9), C6015002, 2016 | 34 | 2016 |
| Revisiting electrochemical techniques to characterize the solid-state diffusion mechanism in lithium-ion batteries IO Santos-Mendoza, J Vázquez-Arenas, I González, G Ramos-Sánchez, ... International Journal of Chemical Reactor Engineering 17 (6), 20180095, 2019 | 32 | 2019 |
| Whole cell bioconversion of (+)‐valencene to (+)‐nootkatone by Yarrowia lipolytica using a three phase partitioning bioreactor DM Palmerín‐Carreño, CO Castillo‐Araiza, OM Rutiaga‐Quiñones, ... Journal of Chemical Technology & Biotechnology 91 (4), 1164-1172, 2016 | 31 | 2016 |
| Mathematical model of a three phase partitioning bioreactor for conversion of ketones using whole cells R Melgarejo-Torres, CO Castillo-Araiza, A Dutta, G Bény, ... Chemical Engineering Journal 260, 765–775, 2014 | 26 | 2014 |
| Effect of diffusion on the conceptual design of a fixed-bed adsorber CO Castillo-Araiza, G Che-Galicia, A Dutta, G Guzmán-González, ... Fuel 149, 100–108, 2015 | 25 | 2015 |
| On the conceptual design of a partitioning technology for the bioconversion of (+)-valencene to (+)-nootkatone on whole cells: Experimentation and modelling CO Castillo-Araiza, D Palmerín-Carreño, A Prado-Barragán, ... Chemical Engineering and Processing: Process Intensification 122, 493-507, 2017 | 23 | 2017 |
| The role of catalyst activity on the steady state and transient behavior of an industrial-scale fixed bed catalytic reactor for the partial oxidation of o-xylene on V2O5/TiO2 … CO Castillo-Araiza, F López-Isunza Chemical Engineering Journal 176, 26-32, 2011 | 23 | 2011 |
| Framing a Novel Approach for Pseudo Continuous Modeling using Direct Numerical Simulations (DNS): Fluid Dynamics in a Packed Bed Reactor A Hernandez-Aguirre, E Hernandez-Martinez, F López-Isunza, ... Chemical Engineering Journal 429, 132061, 2022 | 22 | 2022 |
| Improving ozonation to remove carbamazepine through ozone-assisted catalysis using different NiO concentrations. T Aguilar, C. M., Vazquez-Arenas, J., Castillo-Araiza, C. O., Rodríguez, J ... Environmental Science and Pollution Research., 1-11., 2020 | 22* | 2020 |
| Kinetic, oxygen mass transfer and hydrodynamic studies in a three-phase stirred tank bioreactor for the bioconversion of (+)-valencene on Yarrowia lipolytica 2.2 ab DM Palmerín-Carreño, CO Castillo-Araiza, OM Rutiaga-Quiñones, ... Biochemical engineering journal 113, 37-46, 2016 | 22 | 2016 |
Sergio Huerta-OchoaUniversidad Autónoma Metropolitanaxanum.uam.mx의 이메일 확인됨